CN1092438A - Fluoroelastomer composition - Google Patents

Fluoroelastomer composition Download PDF

Info

Publication number
CN1092438A
CN1092438A CN94100609A CN94100609A CN1092438A CN 1092438 A CN1092438 A CN 1092438A CN 94100609 A CN94100609 A CN 94100609A CN 94100609 A CN94100609 A CN 94100609A CN 1092438 A CN1092438 A CN 1092438A
Authority
CN
China
Prior art keywords
perfluor
vinyl ether
terpolymer
composition
compound
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN94100609A
Other languages
Chinese (zh)
Inventor
齐藤智
达春美
村多弘明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Mektron KK
Original Assignee
Nippon Mektron KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Mektron KK filed Critical Nippon Mektron KK
Publication of CN1092438A publication Critical patent/CN1092438A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/17Amines; Quaternary ammonium compounds
    • C08K5/18Amines; Quaternary ammonium compounds with aromatically bound amino groups

Abstract

A kind of fluoroelastomer composition is provided, it be a kind ofly enable with good selection rate, synthetic cross-linking part monomer carries out the multipolymer of copolymerization at an easy rate, use general commercially available, aspect security also no problem linking agent, form the fluoroelastomer composition of vulcanized rubber with good processibility transitivity.It is in the terpolymer of tetrafluoroethylene, perfluor (low alkyl group vinyl ether) and perfluor (ω-cyano group alkyl vinyl ether), cooperated as stiffening agent, (X, Y: hydroxyl or amino, the meaning of the representative of A is seen described in the specification sheets with following chemical formula.) expression two (aminophenyl) compound.

Description

Fluoroelastomer composition
The present invention relates to fluoroelastomer composition.Relating to a kind of containing with cyano group in more detail is the crosslinkable composite of the fluoroelastomer of bridging property base.
Open on the clear 59-109546 communique the spy, put down in writing a kind of fluoroelastomer composition, said composition is at tetrafluoroethylene, perfluor (methylvinylether) and uses following chemical formula:
In the terpolymer of the cyano group (perfluoroalkyl vinyl ether) of expression, cooperated with two (aminophenyl) compound and made as stiffening agent, wherein, the following chemical formulation of two (aminophenyl) compound
(wherein, A is that carbonatoms is 1~6 a alkylidene group, and carbonatoms is 1~10 perfluorinated alkylidene, SO 2Base, O is basic, CO is basic or make the direct bonded carbon-to-carbons of 2 phenyl ring is hydroxyl or amino in conjunction with, X and Y).
But, the cyano group (perfluoroalkyl vinyl ether) that carries out copolymerization as the cross-linking part monomer (frame Bridge サ イ ト Unit measures body) of above-mentioned terpolymer is as at United States Patent (USP) the 4th, 138, disclosed in No. 426 specification sheetss, need to synthesize through many steps, therefore, being can not be at the raw material of industrial widespread use.In addition, compression set can not meet the demands during high temperature.
On the other hand,, in No. 186 specification sheetss, also disclose following method, that is, in tetrafluoroethylene and perfluor (methylvinylether), used chemical formula to be at United States Patent (USP) the 3rd, 546
Represented perfluor (ω-cyano group alkyl vinyl ether) is the cross-linking part monomer, the terpolymer that carries out copolymerization, this crosslinkedly carry out with tin tetraphenyl.
As the used above-mentioned perfluor of the comonomer composition of this terpolymer (ω-cyano group alkyl vinyl ether), because it can be from its pairing carboxylicesters, with good selection rate, synthesize at an easy rate, so, be the compound that can utilize suitability for industrialized production to obtain, still, because its resulting terpolymer crosslinked is by using tin tetraphenyl, produce that the cyclisation terpolymer of cyano group is incompatible to be carried out.Therefore, not only must be for example under 160 ℃ temperature, such adding for a long time in 18 hours depress sulfuration, and, in addition, also to do promotor etc. with the tin tetraphenyl of strong toxicity as linking agent with the silver suboxide of high price.With regard to crosslinked this point, be conspicuous in the existing problem of industrial application for it.Also have, compression set can not meet the demands when high temperature.
The objective of the invention is to, a kind of fluoroelastomer composition is provided, it is a kind of multipolymer that synthetic cross-linking part monomer carries out copolymerization that allows to carry out with good selection rate, at an easy rate, use general commercially available linking agent also no problem aspect security, form the fluoroelastomer composition of vulcanized rubber with good processibility transitivity.
Following fluoroelastomer composition by made has reached purpose of the present invention, and said composition is at tetrafluoroethylene, perfluor (low alkyl group vinyl ether) and with following chemical formula
In the terpolymer of the perfluor (ω-cyano group alkyl vinyl ether) of (wherein, n is 2~12 integer) expression, cooperated two (aminophenyl) compound stiffening agent to make, wherein, the following chemical formulation of two (aminophenyl) compound,
Figure 941006093_IMG5
(wherein, A is that carbonatoms is that 1~6 alkylidene group, carbonatoms are 1~10 perfluorinated alkylidene, SO 2The base, O is basic, CO is basic or make the combination of 2 direct bonded carbon-to-carbons of phenyl ring, X and Y are hydroxyl or amino).
Terpolymer for tetrafluoroethylene, perfluor (low alkyl group vinyl ether) and perfluor (ω-cyano group alkyl vinyl ether), about 30~75% moles tetrafluoroethylene and about 70~30% moles perfluor (low alkyl group vinyl ether) are carried out in the material of copolymerization, use about 0.5~5% mole, preferred 1~2% mole perfluor (ω-cyano group alkyl vinyl ether) makes it carry out copolymerization as the cross-linking part monomer.In this terpolymer, also can use do not hinder copolymerization and, do not damage the various vinyl compounds of degree of sulfuration rerum natura and the component of fluoridizing (chain) alkene (hydrocarbon) etc. and carry out copolymerization.
Copolymerization can use free-radical initiator, by the letex polymerization in water medium, suspension polymerization, perhaps the solution polymerization in the perfluorochemical solvent carries out, but,, preferably adopt emulsion polymerization in order to obtain more high-molecular weight terpolymer.
For the letex polymerization in water medium, can use ammonium persulphate, the free-radical initiator of Potassium Persulphate etc., these free-radical initiators, with match by reductive agents such as the ammonium salt of sulfurous acid, thiosulfuric acid etc., sodium salt, sylvite, also can be used as redox system and use.For emulsifying agent, generally can use by the ammonium salt of fluoridized carboxylic acid, especially preferably use ammonium perfluorocaprylate.In addition, generally also can use Na 2HPO 4, NaH 2PO 4, K 2HPO 4, KH 2PO 4Deng pH value conditioning agent.
Copolymerization, can be by behind the reactor that quantitative each monomer is once packed into, make it carry out the once adding polymerization process of polyreaction, perhaps, under certain pressure, the any method that evenly adds respectively in the polymerization process that various monomers is respectively charged into according to a certain percentage reactor is carried out, but, in order to obtain having the multipolymer of good rerum natura, the preferred polymerisation process that adopts the latter, polymerization pressure under this occasion that evenly adds respectively remains on about 2~50Kg/cm 2, in addition, polymerization temperature remains on about 40~80 ℃.
After polyreaction ended, with resulting water-based latex, the aqueous solution of the water-soluble electrolyte substance by sodium-chlor, magnesium chloride etc. was saltoutd, by filter, dry, can obtain terpolymer, can not saltout yet, water-based latex is freezing, and with its filtration, drying.
For in terpolymer, cooperated, with represented two (aminophenyl) linking agent of above-mentioned chemical formula, can with about 0.5~5 weight part, be preferably the ratio of about 1~2 weight part according to terpolymer to per 100 weight parts, use for example following compound
Figure 941006093_IMG6
[making two (amino-phenol) AF] with postscript
Figure 941006093_IMG7
Be in the fluoroelastomer composition of neccessary composition with above-mentioned each composition, can suitably cooperate carbon black, the oxide compound of mineral fillers such as silicon-dioxide, divalent metal, oxyhydroxide, stearate, yellow lead oxide etc. are subjected to sour agent (being subjected to sour agent) and other necessary Synergist S-421 95.The modulation of composition is mixing by using the open type roll to wait to carry out, it is crosslinked to be by under about 160~250 ℃ temperature, heats to carry out in about 10~60 minutes.Carrying out the sulfurized occasion twice, preferably in the inert atmosphere of nitrogen etc., carrying out.
Can provide a kind of fluoroelastomer composition by the present invention, it is a kind of multipolymer that synthetic cross-linking part monomer carries out copolymerization that enables to carry out with good selection rate, at an easy rate, use general commercially available, aspect security also no problem linking agent, form the fluoroelastomer composition of vulcanized rubber with good workability transitivity.
[embodiment]
Below, the present invention will be described by embodiment.
Reference example 1
At capacity is in the autoclave of stainless steel of 500ml, the 200ml distilled water of packing into, the Na of the ammonium perfluorocaprylate of 2.5g and 4.4 grams 2HPO 4, 12H 2After the O,, then, reduce pressure its inner nitrogen replacement of using.Again this autoclave is cooled to approximately-50 ℃, then, the order following component of packing into:
Perfluor (5-cyano group amyl group vinyl ether) [FCVE] 6.4g
Perfluor (methylvinylether) [FMVE] 72g
Tetrafluoroethylene [TFE] 32g
After making it be warmed up to 50 ℃, again 0.75g S-WAT and 3.75g ammonium persulphate are made respectively in the 25ml aqueous solution adding autoclave, made it begin to carry out polyreaction.Proceed after 20 hours the polyreaction, with unreacted air scavenge, then, will take out at this formed water-based latex, and saltout, drying obtains the terpolymer A of 18.0g white rubber shape.
This terpolymer A, by the result of infrared spectra absorption analysis, the characteristic absorption that it contains the FCVE(itrile group of 69.5% mole TFE, 30.3% mole FMVE and 0.2% mole is 2268cm -1) multipolymer form.
Reference example 2
To change into 8.2g, 83g and 28g respectively in the FCVE in the reference example 1, FMVE and TFE three's amount, when polymerization begins back 8 hours, add the sodium sulfite aqueous solution and the ammonium persulfate aqueous solution of equal amts again.The terpolymer B of resulting white rubber shape is 36.4g, and its copolymerization consists of 61.8% mole TFE, 37.7% mole FMVE and 0.5% mole FCVE.
Reference example 3
Polymerization temperature in the reference example 2 is changed into 65 ℃, thereby obtain the terpolymer C of 41.5g white rubber shape.Its copolymerization consists of 58.6% mole TFE, 40.7% mole FMVE and 0.7% mole FCVE.
Reference example 4
The amount of FCVE in the reference example 2 is changed into 12.1g, and polymerization temperature is changed into 65 ℃, thereby obtains the terpolymer D of the white rubber shape of 31.2g.Its copolymerization consists of 62.1% mole TFE, 36.8% mole FMVE and 1.1% mole FCVE.
Reference example 5
The amount of FCVE in the reference example 2 is changed into 16.4g, and polymerization temperature is changed into 65 ℃, thereby obtains the terpolymer E of the white rubber shape of 22.4g.Its copolymerization consists of 67.7% mole TFE, 30.8% mole FMVE and 1.5% mole FCVE.
Reference example 6
At capacity is in the autoclave of stainless steel of 3L, the distilled water of the 1.57L that packs into, the ammonium perfluorocaprylate of 27.3g and the Na of 23.7g 2HPO 4, 12H 2After the O,, then, reduce pressure its inner nitrogen replacement of using.Again autoclave is cooled to-50 ℃, then, the following component of packing in proper order:
Tetrafluoroethylene [TFE] 30g
Perfluor (methylvinylether) [FMVE] 50g
Perfluor (5-cyano group amyl group vinyl ether) [FCVE] 4.6g
It is warmed up to after 60 ℃,, makes the aqueous solution of 50ml respectively, add in the autoclave, make it begin to carry out polyreaction again with the S-WAT of 1.66g and the ammonium persulphate of 9.08g.
In polyreaction, be that 27g/ hour, FMVE are that 43g/ hour, FCVE are that 4.0g/ hour flow adds respectively with TFE, the pressure in the autoclave is remained on 9Kg/cm 2After beginning polymerization 10 hours, stop to add respectively, in addition, kept in this state 1 hour.Make the autoclave cooling, get rid of residual gas, then, take out water-based latex.
The water-based latex (concentration of solids component is 28% weight) that is taken out is freezing, and with 10% washing with alcohol, under 70 ℃ of temperature after the constant pressure and dry 12 hours, again under 120 ℃ temperature, drying under reduced pressure 8 hours, thus the terpolymer F of the white rubber shape of 700g obtained.Its copolymerization consists of 55.9% mole TFE, 42.7% mole FMVE, 1.4% mole FCVE.In addition, its reduced viscosity is η SP/ C[measures under 35 ℃ for perfluor (2-butyl tetrahydrofuran) solution of 1% weight] be 1.04ml/g.
Embodiment 1
With following various gradation compositions:
Terpolymer A 100 weight parts
Two (amino-phenol) AF, 2 weight parts
Dicyclohexyl-hexaoxacyclooctadecane-6-6 0.5 weight part
MT carbon black 10 weight parts
Yellow lead oxide 2 weight parts
On two roller rubber milling trains, carry out mixingly, under 180 ℃ temperature, carry out 15 minutes press vulcanization,, measure the sulfuration moment of torsion with キ ユ ラ ス ト メ--レ (オ リ エ Application テ シ Network System), the 0.5kgcm that risen as can be seen, thus its sulfuration obtains confirming.
Embodiment 2~4
With the terpolymer A among the embodiment 1, replace with terpolymer C, D or E with amount, under 180 ℃ temperature, carry out once (pressurization) sulfuration of one hour, and under 250 ℃ temperature, carrying out 24 hours secondary (baker) sulfuration, the physics value of resulting sulfur product is shown in the following table 1 with the moment of torsion ascensional range.
Table 1
Embodiment 2 embodiment 3 embodiment 4
Terpolymer C D E
Moment of torsion ascensional range (kgcm) 3.1 3.9 4.8
Breaking tenacity (kgf/cm 2) 175 182 180
Extension at break (%) 220 173 160
Embodiment 5~6
With following various gradation compositions:
Terpolymer F 100 weight parts
Two (amino-phenol) AF, 1 weight part (embodiment 5)
2 weight parts (embodiment 6)
MT carbon black 20 weight parts
On two roller rubber milling trains, carry out mixing, under 180 ℃ temperature, carry out once (pressurization) sulfuration of 30 minutes, and under 210 ℃ temperature, carried out 18 hours and under 288 ℃ temperature, carried out 18 hours 2 stage secondaries (baker) sulfuration, the normality rerum natura of resulting sulfur product and compression set (ASTM method B, p24, O type ring: 275 ℃, 70 hours), list in the table 2 simultaneously with the moment of torsion ascensional range.
Table 2
Embodiment 5 embodiment 6
Moment of torsion ascensional range (kgcm) 9.3 11.9
Hardness (JIS A) 76 78
100% modulus (Kgf/cm 2) 92 132
Breaking tenacity (Kgf/cm 2) 192 194
Extension at break (%) 180 130
Compression set (%) 22 13
Comparative example
With following each gradation composition
Cooperate (weight part) to cooperate formula I to cooperate formula I I
Terpolymer B 100 100
Tin tetraphenyl 6
MT carbon black 10 10
Silver suboxide 4.8
On two roller rubber milling trains, carry out mixingly, under 180 ℃ temperature, carry out 2 hours sulfuration, do not find the rising of the sulfuration torque value on キ ユ ラ ス ト メ--V fully.

Claims (4)

1, a kind of fluoroelastomer composition, said composition are at tetrafluoroethylene, perfluor (low alkyl group vinyl ether) and use chemical formula CF 2=CFO (CF 2) nCN is (in the formula, n is 2~12 integer) in the terpolymer of represented perfluor (ω-cyano group alkyl vinyl ether), cooperated two (aminophenyl) compound to form as stiffening agent, wherein, the following chemical formulation of two (aminophenyl) compound:
Figure 941006093_IMG2
(wherein, A is that carbonatoms is 1~6 alkylidene group, and carbonatoms is 1~10 perfluorinated alkylidene, SO 2Base, O is basic, CO is basic or make the direct bonded carbon-to-carbons of 2 phenyl ring is hydroxyl or amino in conjunction with, X and Y).
2, the described fluoroelastomer composition of a kind of claim 1, said composition is the terpolymer of tetrafluoroethylene, perfluor (low alkyl group vinyl ether) and perfluor (ω-cyano group alkyl vinyl ether), it is that about 30~70% moles tetrafluoroethylene and about 70~30% moles perfluor (low alkyl group vinyl ether) are carried out in the material of copolymerization, and (ω-cyano group alkyl vinyl ether) carries out the polymeric co-polymer as the cross-linking part monomer with about 0.5~5% mole perfluor.
3, the described fluoroelastomer composition of a kind of claim 1, wherein, stiffening agent two (aminophenyl) compound is the compound shown in the following chemical formula.
Figure 941006093_IMG3
4, a kind of claim 1 or 3 described fluoroelastomer compositions, the cooperation ratio of stiffening agent two (aminophenyl) compound of said composition with respect to the terpolymer of 100 weight parts, is about 0.5~5 weight part.
CN94100609A 1993-01-14 1994-01-14 Fluoroelastomer composition Pending CN1092438A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2196393 1993-01-14
JP021963/93 1993-01-14

Publications (1)

Publication Number Publication Date
CN1092438A true CN1092438A (en) 1994-09-21

Family

ID=12069720

Family Applications (1)

Application Number Title Priority Date Filing Date
CN94100609A Pending CN1092438A (en) 1993-01-14 1994-01-14 Fluoroelastomer composition

Country Status (4)

Country Link
US (1) US6602961B1 (en)
EP (1) EP0606883B1 (en)
CN (1) CN1092438A (en)
DE (2) DE69413854T2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1315894C (en) * 2002-05-02 2007-05-16 杜邦唐弹性体公司 Curable base-resistant fluoroelastomers
CN100338108C (en) * 2002-03-14 2007-09-19 大金工业株式会社 Fluorocopolymer, process for producing fluorocopolymer, curable fluorocopolymer composition, and cured object
CN1891761B (en) * 2001-12-17 2010-10-06 大金工业株式会社 Crosslinkable elastomer composition and formed product comprising the same
CN101563375B (en) * 2006-12-21 2011-10-05 纳幕尔杜邦公司 Crosslinkable vinyl fluoride copolymers
CN102858871A (en) * 2010-04-29 2013-01-02 纳幕尔杜邦公司 Manufacture of perfluoroelastomer compounds containing fibrillating PTFE
CN109715718A (en) * 2016-07-18 2019-05-03 索尔维特殊聚合物意大利有限公司 Fluoroelastomer composition

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08104789A (en) * 1994-10-04 1996-04-23 Nippon Mektron Ltd Fluorine-containing elastomer composition
US5824749A (en) * 1994-10-04 1998-10-20 Nippon Mektron, Limited Fluorine-containing elastomer composition
JP2833645B2 (en) * 1994-10-21 1998-12-09 日本メクトロン株式会社 Fluorine-containing elastomer composition
JP3398492B2 (en) * 1994-10-21 2003-04-21 日本メクトロン株式会社 Fluorine-containing elastomer composition
JPH08143535A (en) * 1994-11-17 1996-06-04 Nippon Mektron Ltd Bisaminothiophenol compound, its production and curing agent for elastomer containing fluorine comprising the same
JP2891294B2 (en) * 1995-07-13 1999-05-17 日本メクトロン株式会社 Fluorine-containing elastomer composition
US5936060A (en) * 1996-11-25 1999-08-10 E. I. Du Pont De Nemours And Company Perfluoroelastomer composition having improved processability
US5874523A (en) * 1996-11-25 1999-02-23 E. I. Du Pont De Nemours And Company Sulfonated perfluoroelastomer composition having improved processability
US6114452A (en) * 1996-11-25 2000-09-05 E. I. Du Pont De Nemours And Company Perfluoroelastomer composition having excellent heat stability
WO1998023655A1 (en) * 1996-11-25 1998-06-04 E.I. Du Pont De Nemours And Company Perfluoroelastomer composition having improved processability
JP4602555B2 (en) 1998-11-13 2010-12-22 ダイキン工業株式会社 Fluorine-containing elastomer and composition for crosslinking
WO2000042100A1 (en) * 1999-01-12 2000-07-20 Daikin Industries, Ltd. Crosslinkable elastomer composition and formed article prepared from said composition
JP4240716B2 (en) * 1999-02-01 2009-03-18 ユニマテック株式会社 Fluorine-containing elastomer composition
US6956085B2 (en) * 2003-02-14 2005-10-18 3M Innovative Properties Company Fluoroelastomer compositions
JP4687650B2 (en) * 2004-04-28 2011-05-25 ダイキン工業株式会社 Fluorine-containing elastomer composition and molded article comprising the same
WO2012040250A2 (en) 2010-09-24 2012-03-29 Greene, Tweed Of Delaware, Inc. Fluorine-containing elastomer compositions suitable for high temperature applications
US9365712B2 (en) 2010-09-24 2016-06-14 Greene, Tweed Technologies, Inc. Fluorine-containing elastomer compositions suitable for high temperature applications
KR101976232B1 (en) 2011-11-09 2019-05-07 쓰리엠 이노베이티브 프로퍼티즈 컴파니 Curing compositions for fluoropolymers

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3114778A (en) * 1963-12-17 Fluorinated vinyl ethers and their
GB1145445A (en) * 1966-02-16 1969-03-12 Du Pont Fluorinated perfluorovinylethers, their preparation and copolymers thereof
US4131740A (en) 1977-04-20 1978-12-26 E. I. Du Pont De Nemours And Company Alkyl perfluoro-ω-fluoroformyl esters and their preparation
US4525539A (en) 1982-12-02 1985-06-25 E. I. Du Pont De Nemours And Company Vulcanizable nitrile-containing perfluoroelastomer
US4529784A (en) * 1983-07-11 1985-07-16 E. I. Du Pont De Nemours And Company Fluorinated copolymers with improved cure site
JPS62260807A (en) * 1986-05-07 1987-11-13 Nippon Mektron Ltd Fluorine-containing polymer and fluorine-containing polymer composition

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1891761B (en) * 2001-12-17 2010-10-06 大金工业株式会社 Crosslinkable elastomer composition and formed product comprising the same
CN100338108C (en) * 2002-03-14 2007-09-19 大金工业株式会社 Fluorocopolymer, process for producing fluorocopolymer, curable fluorocopolymer composition, and cured object
US7538170B2 (en) 2002-03-14 2009-05-26 Daikin Industries, Ltd. Fluorocopolymer, process for producing fluorocopolymer, fluorocopolymer curable composition, and cured object
US7915361B2 (en) 2002-03-14 2011-03-29 Daikin Industries, Ltd. Fluorocopolymer, process for producing fluorocopolymer, fluorocopolymer curable composition, and cured object
CN1315894C (en) * 2002-05-02 2007-05-16 杜邦唐弹性体公司 Curable base-resistant fluoroelastomers
CN101563375B (en) * 2006-12-21 2011-10-05 纳幕尔杜邦公司 Crosslinkable vinyl fluoride copolymers
CN101558092B (en) * 2006-12-21 2011-11-16 纳幕尔杜邦公司 Crosslinkable vinyl fluoride copolymer coated film and process for making same
CN102858871A (en) * 2010-04-29 2013-01-02 纳幕尔杜邦公司 Manufacture of perfluoroelastomer compounds containing fibrillating PTFE
CN109715718A (en) * 2016-07-18 2019-05-03 索尔维特殊聚合物意大利有限公司 Fluoroelastomer composition
CN109715718B (en) * 2016-07-18 2021-09-21 索尔维特殊聚合物意大利有限公司 Fluoroelastomer composition

Also Published As

Publication number Publication date
US6602961B1 (en) 2003-08-05
EP0606883B1 (en) 1998-10-14
EP0606883A1 (en) 1994-07-20
DE69413854D1 (en) 1998-11-19
DE69413854T2 (en) 1999-04-01
DE606883T1 (en) 1995-03-16

Similar Documents

Publication Publication Date Title
CN1092438A (en) Fluoroelastomer composition
CN1297578C (en) Peroxide curable fluoroelastomers
EP2601226B2 (en) Peroxide curable fluoroelastomers containing modifiers and iodine or bromine endgroups
CN1100821C (en) Curable eluoroelastomeric compositions
JP3103386B2 (en) Fluor elastic body and manufacturing method thereof
CN1100820C (en) Fluorine-containing elastomer composition
CN100441605C (en) Perfluoroelastomer compsns.
US5648429A (en) Curable fluoroelastomeric compositions
CN102007150B (en) There is the Perfluoroelastomer of low carbonyl endgroup ratios
CN87103158A (en) The polymerization process of fluorinated monomer in aqueous dispersions
CN1006891B (en) Process for the preparation of curable flouroelastomers and products go obtained
CN1553934A (en) Peroxide curable fluorelastomer compositions
CN1152583A (en) Peroxide crosslinkable fluororubbers, process for production thereof and use thereof
CN1063742C (en) Bisamidrazone compound and vulcanizing agent for fluorine-containing elastomer comprising the same
JPH073101A (en) Fluoroelastomer composition
CN1743352A (en) Polyurethane and its complex substance in-situ modified polyvinyl chloride resin and preparing method
CN1461313A (en) Process for producing high-strength tetrafluoroethylene polymer
CN1910203A (en) Fluoropolymer coagulation method and composition
CA2096673C (en) Fluoroelastomeric and fluoroplastomeric copolymers having a high resistance to bases
CN1169739A (en) Fluorine-containing polymers and preparation thereof
CN1834126A (en) Method of adopting template copolymerization process for synthetizing hydrophobic associated water-soluble polymer
US6124404A (en) Process for producing fluorine-containing graft copolymer
JP3375404B2 (en) Fluorine-containing elastomer composition
JPH07118348A (en) Nitrogenous fluorocarbon copolymer, its production and its use
CN1711287A (en) Process for making a fluoropolymer having nitrile end groups

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication